KR200314901Y1 - Wastewater disposal plant - Google Patents

Abstract

The present invention relates to a wastewater treatment apparatus, which will be described in detail. Nitrogen treatment efficiency of the organic matter and nitrogen contained in the wastewater into a biofilm (MLSS) adsorbed to a carrier without floating microorganisms in one contact aeration tank is described. The present invention relates to a wastewater treatment apparatus for strengthening the wastewater, comprising: a screen process for treating solid matter and large suspended solids contained in the influent, and a flow rate for adjusting the concentration and flow rate of pollutants in the wastewater that have passed through the screen process. After the adjustment process and the flow rate adjustment process, it consists of an integrated process (contact aeration tank) to remove nitrogen components and organic matter contained in the influent water by using the biofilm (MLSS) attached to the carrier, the biofilm (MLSS) attached to the carrier ) A backwashing device, a backwashing device, and a needle to increase the treatment efficiency by detaching the biofilm (MLSS) attached to the carrier. Sludge drawing device for drawing the sludge from the tank bottom (floor); by configuring the biological oxygen demand of contamination there is an effect that the nitrogen removes more than 90% (5mg / ℓ) can be removed up to 90% or more.

Description

Wastewater treatment system that adsorbs and grows biofilm to enhance nitrogen treatment efficiency {WASTEWATER DISPOSAL PLANT}

The present invention develops a new type of biofilm that adsorbs and grows organic pollutants (BOD), suspended solids (SS) and nitrogen components contained in wastewater and can be simultaneously carried out in one integrated process using only biofilms (MLSS). The present invention relates to a wastewater treatment apparatus which has been adsorbed and grown to enhance nitrogen treatment efficiency.

In general, pollutants present in sewage, sewage, and wastewater (hereinafter referred to as influent) are being treated by physical, chemical, and biological methods.

Representative systems for treating conventional influent water are firstly removed from the screen tank (1) to remove the large particles of solids and suspended solids contained in the influent as shown in Figure 1 and the concentration of contaminants in the flow control tank (2) And the flow rate are adjusted equally, then settling in the primary settling tank (3), and then sequentially in the anoxic tank (4) and activated sludge tank

(5) and the secondary sedimentation tank (6), and the aeration method of activated sludge is the organic contaminant contained in the influent water as a nutrient component to proliferate while decomposing by oxidation, adsorption, self-oxidation and at the same time In the anoxic tank (4) of the nitrogen sludge was removed by reducing the nitrated nitrogen in the internal circulating water passed through the activated sludge tank (5), and then in the secondary precipitation tank (6) to precipitate the activated sludge to separate from the supernatant, and to the supernatant The treated water is disinfected and discharged in the discharge tank (7), a part of the activated sludge precipitated in the secondary precipitation tank (6) is returned to the activated sludge tank (5) and the excess sludge is sludge storage tank

It is composed of a system that is sent to the city for disposal, and because each process is installed independently, it is not only expensive to install and operate, but also difficult to manage, and does not show satisfactory efficiency of organic matter and nitrogen treatment. There is a problem.

By the way, in the fibrous carrier installed in the fixed phase of the conventional wastewater treatment system as described above, a fixed-phase carrier in which microorganisms adhere to fibers having a large specific surface area constitutes the mainstream. In the wastewater treatment system exhibiting a severe deviation in each time zone, there is a problem in that desorption is easy due to the physical force caused by the shear stress, and the response force of the system to the load fluctuation is weak.

In addition, the conventional wastewater treatment system has a short residence time of activated sludge, which makes it difficult to process hardly decomposable substances and is not sufficient for growth of nitrifying microorganisms, which generally slow microbial growth, and frequently cause abnormalities such as sludge bulking. There is a drawback of low efficiency of the treatment of gas and nitrogen.

Therefore, the object of the present invention is to solve such a problem, the object of the present invention is to treat nitrogen and organic matter contained in the influent in a single integrated process by treating only the biofilm adsorbed on the carrier without floating microorganisms (MLSS) The present invention provides a method for enabling altitude processing and an easy operation management technique.

In addition, another object of the present invention is to install and apply a multi-layered carrier in the contact aeration tank to facilitate the adsorption, oxidation, reduction and self-decomposition in the integrated treatment process to increase the efficiency of waste water, especially nitrogen treatment. To provide a waste water treatment system that can be.

1 is a system configuration diagram of a conventional wastewater treatment apparatus.

2 is a process chart of the waste water treatment apparatus according to the present invention.

Figure 3 is a schematic diagram showing the configuration of the waste water treatment apparatus according to the present invention.

4 is a view showing a carrier of FIG.

Explanation of symbols on the main parts of the drawings

S1: Screen process S2: Flow adjustment process S3: Integrated treatment process S4: Precipitation process S5: Discharge process 10: Screen bath

20: flow rate adjustment tank 30: contact aeration tank 40: sedimentation tank 50: discharge tank 60: sludge storage tank 70: screen

80,140,150: Uharain 90: Operator's Organization 100: Influent Transfer Line 110: Reverse Taxation Engine 120: Carrier 130: Domestic Circulation Line 142: Sludge Drawing Line 152: Backwashing Line 160: Supernatant Water Line

The present invention relates to a wastewater treatment apparatus for adsorbing and growing a biofilm to enhance nitrogen treatment efficiency. The present invention relates to a conventional screen process for filtering solid matter present in influent water, and a flow rate and contaminant concentration of influent water through the screen process. Adsorption, oxidation, reduction, and the like in a conventional flow rate adjusting step for adjusting and a biofilm (MLSS) which adsorbs (attaches) and propagates organic matter, suspended matter, and nitrogen contained in the influent water uniformed in the flow rate adjusting step. And an integrated treatment process for self-oxidation, a precipitation process for backwashing and precipitating the biofilm (MLSS) adsorbed on the carrier, a discharge process for discharging the treated water treated with the influent, and a extraction and storage of all the sludge precipitated and deposited. The sludge storage process is characterized in that the influent is purified.

In addition, as a device for achieving the waste water treatment according to the present invention is a microorganism that is adsorbed, oxidized, reduced, and self-decomposed in an integrated treatment process (contact aeration tank) to remove organic matter and nitrogen components in the influent water Contact aeration tank where carriers are stacked, sedimentation tank which precipitates sludge desorbed during operation and backwashing, acid engine which aeration of contact aeration tank and backwashing engine which desorbs biofilm attached to carrier, internal circulation to increase nitrogen treatment efficiency It is another feature that the line is further provided.

With reference to the accompanying drawings, the wastewater treatment apparatus according to the present invention will be understood by the embodiments described in detail below.

2 is a process diagram of the wastewater treatment apparatus according to the present invention, Figure 3 is a schematic view of the configuration of the wastewater treatment apparatus according to the present invention, Figure 4 is a view showing the carrier portion of FIG.

Referring to Figure 2 briefly described the process sequence of the wastewater treatment apparatus of the present invention.

First, the wastewater treatment process includes a screen process (S1) for filtering large particles and suspended solids present in the influent and a flow rate for adjusting the contaminant concentration and the flow rate of the influent introduced through the screen process (S1). Adsorption (adhering) to the carrier to be described later after the integrated processing step (S3) and the integrated processing step (S3) for removing organic matter, suspended matter and nitrogen in the influent water uniformized in the adjusting step (S2) and the flow rate adjusting step (S2). ) And a settling step (S4) of precipitating and detaching the biofilm (MLSS) and a discharge step (S5) of discharging the treated water after the settling step (S4).

In each process, the process of removing contaminants contained in the influent, for example, BOD, nitrogen, and other components, is in charge of the integrated treatment process (S3). will be.

Hereinafter, with reference to Figures 2 to 4 will be described a specific configuration of the waste water treatment apparatus according to the present invention.

The integrated processing step (S3) is made in the contact aeration tank 30, the contact aeration tank is composed of a plurality of aeration tanks (30a, 30b, 30c, 30d) in series, the aeration tank (30a) is an oxygen-free tank the remaining aeration tank (30b) , 30c, 30d are the reaction tank 3

Based on 0), the aeration tank 30a becomes an upstream aeration tank and the aeration tank 30d becomes a downstream aeration tank.

The sedimentation tank 40 precipitates some suspended solids (SS) contained in the treated water and settles the sludge generated during backwashing in the aeration tanks 30b, 30c, and 30d, and then the sludge storage tank.

Processed water is sent to the discharge tank 50, which is the discharge process through the outlet line 150 to send to (60).

An diffuser is installed inside the contact aeration tank 30. The diffuser is blown to the air line 170, thereby supplying air into the contact aeration tank 30, thereby causing aeration.

The diffuser is composed of an operating diffuser (90) for driving and backwashing the bottom of the contact aeration tank (30), which is composed of upward and backward with a backwashing engine (110) for backwashing the carrier (122) to be described later. There is, the driving engine 90 and the back-counter engine 110 is installed to maintain a certain distance.

In the contact aeration tank 30, a carrier portion 120 in which a carrier 122 having a large porosity and a surface area and having a cross-section having a "∧" shape is installed in multiple stages is installed, and a carrier 122 having one end thereof forms a lower layer. ) Is arranged in a plural number in the horizontal direction, the upper end is provided with a second stage in which a plurality of carriers 122 are arranged in a direction orthogonal to the carrier 122 disposed at the one end and the carrier 122 configured at the one end thereof In the same direction as the plurality of carriers 122 are provided in three stages arranged side by side.

The carrier 122 may be composed of any one of three or more stages (four, five, six ...).

As a result, the carrier unit 120 has a plurality of carriers 122 having a plate shape inclined at both ends of the carrier unit 120 to be alternately stacked on the carrier unit 120. A plurality of air holes 124 are perforated to facilitate circulation of the air supplied through the air.

As described above, the carrier part 120 is fixed to the outside of the carrier part 120 in which the plurality of carriers 120 are stacked in multiple stages with an iron structure (not shown) and a mesh (not shown) such that the carrier part 120 does not move. This is preferable.

On the other hand, in order to increase the nitrogen treatment efficiency by installing the internal circulation line 130 in the aeration tank (30d) by the pump (P2) installed in the contact aeration tank (30d) the aeration tank (30a)

Transfer to. The lower part of the sedimentation tank 40 is provided with a sludge drawing line 142 for drawing out the sludge, sedimentation sludge is connected to the pumping line of the pump (P4) installed on one side of the sedimentation tank (40).

Hereinafter, the operation of the present invention and the effects thereof.

The inflow water passing through the screen 70 in the screen tank 10 is stored in the flow rate adjustment tank 20 through the U Haraine 80 and the inflow water transfer line by the pump (P1) installed inside the flow rate adjustment tank 20 ( It is pumped to 100 and flows into the aeration tank (30a).

The aeration tank (30a) inside the aerobic mixing action is accompanied by the air supplied from the diffuser, and in the aeration tank (30d) and the pollutant contained in the inflow water by the carrier 122 stacked in multiple layers It removes contaminants contained in the influent water transferred through the inner circulation line (130).

In the aeration tanks 30b, 30c, and 30d, removal of contaminants that are not decomposed in the aeration tank 30a and adsorption (adhesion) of the nitrifying microorganisms are carried out to nitrate nitrogen components, and the biofilm is enlarged, resulting in floating sludge, thereby lowering treatment efficiency. In order not to periodically operate the backwashing engine 110 and backwashing water.

The treated influent is introduced into the sedimentation tank 40 along the Uharain 140 and the sludge settled below the sedimentation tank 40 is intermittently drawn out, and the sludge drawing line 142 is drawn by drawing all the sludge in backwashing. The sludge is disposed of by transporting the sludge to the sludge storage tank 60, and the supernatant water is transferred to the discharge tank 50 through the Uharain 150 and discharged through the outlet 180.

As such, in order to increase the active capacity of the polymer material secreted by the organism in the aeration tanks 30b, 30c, and 30d, the backwashing organ 110 and the backwashing line are periodically and stepwise.

By supplying backwash water through 152 to activate the adsorption capacity of the biofilm attached to the carrier 122, the floating microorganisms in the aeration tank (30d) is lowered below 10 mg / l.

Although the embodiments of the present invention have been described in detail as described above, the scope of the present invention is not limited thereto, and the scope of the present invention is substantially equivalent to that of the embodiment of the present invention.

To the extent that it extends to the scope of the present invention.

As can be seen from the above description, the wastewater treatment apparatus according to the present invention

It is possible to purify pollutants of small and medium scale, which is expected to contribute greatly to solving environmental pollution problems.

In addition, the waste water treatment apparatus of the present invention has no advantage of the system itself, and there is an advantage in that the structure is simple because both the organic matter and the nitrogen purification treatment are performed in one reaction tank (contact aeration tank).

In addition, it operates without contact aeration tank floating microorganisms (MLSS), so there is no need for a precipitation tank. (In the case of advanced treatment, a precipitation tank is preferable.)

In addition, the biofilm treatment for adsorption and growth of organic matter and nitrogen components contained in the influent according to the present invention to the fixed-phase carrier filled in the aeration tank, so that the anaerobic, oxygen-free, aerobic region coexist in the carrier, the internal circulation device Even if the nitrogen removal rate is high and there is an advantage that the nitrogen removal rate is 10% higher than the above when the internal circulation.

In addition, since the total amount of the sludge concentrated phosphorus in the contact aeration tank is transported to the sludge storage tank for disposal without sedimentation and return, the phosphorus removal efficiency is also satisfactory.

As a result, the present invention can significantly reduce the cost of maintenance and maintenance by installing and improving the treatment efficiency of the conventional activated sludge variation and other contact aeration methods, in particular, the integrated treatment process of the present invention anaerobic aeration tank as in the prior art Compared to the installation separately, the installation area can be reduced by 30% or more, and the apparatus and process can be automated to implement a purification treatment device that is easy to operate and manage.

Claims (5)

The flow rate adjustment tank for adjusting and storing the pollution concentration and flow rate of the inflow water introduced through the inlet port, and the carrier portion for attaching and processing the organic matter, suspended matter and nitrogen components contained in the uniform inflow water through the flow adjustment tank is installed inside In the waste water treatment apparatus having a contact aeration tank, a sedimentation tank for separating the biofilm (MLSS) generated in the contact aeration tank with the treated water, and a discharge tank for discharging the treated water treated in the sedimentation tank, An air line is installed in the wastewater treatment device, and the contact aeration tank is a wastewater treatment device for enhancing nitrogen treatment efficiency by adsorbing and growing a biofilm, characterized in that a plurality of aeration tanks are arranged in series. The method of claim 1, A plurality of carriers are installed in the lower portion of the contact aeration tank, and the backwashing engine consisting of upwards and the operating engine composed of downwards are separated and installed at a predetermined distance, thereby adsorbing and growing a biofilm to enhance nitrogen treatment efficiency. Wastewater Treatment System. The method of claim 2, The carrier has a plate shape inclined at both ends downwardly and alternately stacked, but the carrier is adsorbed and grown biofilm, characterized in that a plurality of air holes perforated, wastewater treatment apparatus to enhance the efficiency of nitrogen treatment. The method of claim 1, The wastewater treatment apparatus is provided with a backwashing line for supplying backwash water from any one of the plurality of aeration tanks from the discharge tank to adsorb and grow a biofilm, thereby enhancing nitrogen treatment efficiency. Processing unit. The method of claim 1, The waste water treatment apparatus is provided with an internal circulation line for circulating the treated water from the aeration tank provided downstream of the plurality of aeration tanks to the aeration tank provided upstream, so that the biofilm is adsorbed and grown to improve nitrogen treatment efficiency. Enhanced wastewater treatment system.